• 대한기계학회:학술대회논문집
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• 대한기계학회 2003년도 추계학술대회
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• pp.1180-1185
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• 2003

One of the main degradation of steam generator tubes is stress corrosion cracking induced by residual stress. The resulting damages can cause tube bursting or leakage of the primary water which contained radioactivity. Primary water stress corrosion crack occurs at the location of tube/tubesheet hard rolled transition zone. In order to investigate the effect of shot peening on stress corrosion cracking, stress intensity factors are calculated for the crack which is located in the induced residual stress field.

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2002년도 추계학술대회 논문집
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• pp.709-712
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• 2002

For the electro-discharge machining of an electro-conductive anisotropic composite, an unsteady state formulation was established and solved by Galerkin's finite element method. The distribution of temperature on work piece, the shape of the crater and the material removal rate were obtained in terms of the process parameters. As the spark was initiated the workpiece immediately started to melt and the heat affected zone was formed. The moving boundary of the crater was also identified with time. When the radial and axial conductivities were increased separately the temperature distribution and the shape of the crater were shifted in the same direction respectively and the material removal rate was found to be higher in the case of increasing radial conductivity rather than the axial conductivity.

• 설비공학논문집
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• 제16권8호
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• pp.698-706
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• 2004

Heat transfer coefficients of enhanced tubes in a flooded evaporator are measured through Wilson Plot method. And the correlations are proposed to design a flooded evaporators. Overall heat transfer coefficients are composed of the heat transfer coefficients both inside and outside tubes. Usually the experiments have been conducted separately. But there have been many difficulties like setting up the equipments and measuring the wall temperature. Wilson Plot method makes it possible to measure the separated transfer coefficients at the same equipment through experimental skills. So the cost and time can be reduced. And the results are reliable enough to use for design. Heat transfer coefficients inside the tube were able to be correlated uniquely in spite of various outside conditions. Boiling heat transfer of R134a is more dependent on the saturation temperature and much higher than that of R123.

• 설비공학논문집
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• 제10권5호
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• pp.509-522
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• 1998

An experimental investigation is reported on the heat transfer coefficient from a rotating flat plate in a round turbulent normally impinging water jet. Tests were conducted over a range of jet flow rates, rotational speeds, jet radial posetions with various combinations of three jet nozzle diameter. Dimensionless correlation of average Nusselt number for laminar and turbulent flow is given in terms of jet and rotational Reynolds numbers, dimensionless jet radial position. We suggested various effective promotion methods according to heat transfer characteristics and aspects. The data presented herein will serve as a first step toward providing the information necessary to optimize in rational manner the cooling requirement of impingement cooled rotating machine components.

• 설비공학논문집
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• 제13권12호
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• pp.1214-1222
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• 2001

The present study investigated the effect of diameter and length on the absorption performance of a vertical falling film type absorber using $LiBr-H_2$O solution of 60 wt%. The parameters were diameter of absorber (17.2, 23.4, 31.1 mm), length of absorber (771, 1150, 1528 mm), and film Reynolds numbers (50, 70, 90, 110, 130, 150). As the diameter of the absorber was increased, the absorption mass flux, Sherwood number, heat flux, and heat transfer coefficient were increased, in which Sherwood number and heat transfer coefficient were increased up to 13% and 30% respectively. As the length of the absorber was increased, the total absorption rate and heat transfer coefficient were increased by 37% and 35% respectively, while the absorption mass flux was decreased.

• 설비공학논문집
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• 제12권12호
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• pp.1081-1089
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• 2000

Evaporating heat transfer coefficients of R-22 and R-134a were measured in smooth horizontal copper tubes with inner diameters of 1.77, 3.36 and 5.35mm, respectively. The experiments were conducted in a closed loop, which was driven by a magnetic gear pump. Experiments were performed for the following range of variables: mass velocity (200 to 400 kg/$m^2$.s), saturation temperature($0^{circ}C,; 5^{\circ}C$) and quality(0 to 1.0). Main results obtained are as follows: evaporating heat transfer coefficients in the small diameter tubes (ID<7mm) were observed to be strongly affected by various diameters and to differ from those in the large diameter tubers. The heat transfer coefficients of the small diameter tubes were higher than those of the large diameter tubs. And it was very difficult to apply some well-known previous predictions (Shah`s, Gungor-Winterton`s and Kandlikar`s correlation) to small diameter tubes.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집A
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• pp.19-24
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• 2000

Stress corrosion crack growth is simulated after assuming a small axial surface crack inside a S/G tube. Internal pressure and residual stresses are considered as applied forces. Stress intensity factors along crack front, variation of crack shape and crack growth rate are obtained and discussed. It is noticed that the aspect ratio of the crack is not depend on the initial crack shape but depend on the residual stress distribution.

• 설비공학논문집
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• 제16권3호
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• pp.280-286
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• 2004

An experimental study is peformed to examine the heat transfer performance of individual rows of fin-tube heat exchangers. The heat transfer performance is measured using an air-enthalpy type calorimeter. The examined heat exchangers consist of 7mm tube and fin patterns of them are slit and louver types. Equivalent fin spacings are 18 fins per inch(fpi) for all samples, and the number of tube rows are two. In order to confirm that thermal boundary condition on fins of each row are the same, physically separated between two rows as well as connected heat exchangers are used. The frontal air velocity is varied from 0.7 to 2.5㎧. Heat transfer performance for each row is measured. It is observed that the heat transfer coefficient of the second row is smaller than that of the first row at low Reynolds number while larger at high Reynolds number.

• 생물환경조절학회지
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• 제24권2호
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• pp.100-105
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• 2015

온실의 난방부하 중 틈새환기전열부하 산정방법은 설계 기준마다 제각각이고, 온실의 규모에 따라 각각의 방법에는 큰 차이가 있으므로 보다 정확히 국내에 적용할 수 있는 방법을 정립할 필요가 있다. 본 연구에서는 원예시설의 환경설계 중 난방부하 산정방법 정립에 필요한 기초자료를 제공할 목적으로 다양한 종류의 보온커튼을 설치한 단동 및 연동 플라스틱 온실에서 추적가스법을 이용하여 틈새환기율을 실측하였으며, 온실의 틈새환기 전열부하 산정방법을 검토하였다. 연동온실의 틈새환기율은 $0.042{\sim}0.245h^{-1}$의 범위로 측정되었으며 단동온실의 틈새환기율은 $0.056{\sim}0.336h^{-1}$의 범위로 측정되어 단동온실이 약간 큰 것으로 나타났다. 온실의 틈새환기율은 단동, 연동 구분없이 보온커튼의 층수에 따라 크게 감소하는 것으로 나타났다. 또한 틈새환기율은 온실의 실내외 기온차가 커질수록 증가하는 경향을 보였으나, 실험기간 동안의 낮은 풍속 범위에서 외부 풍속에 따른 틈새환기율의 변화는 일정한 경향을 찾을 수 없었다. 온실의 난방설계를 위한 틈새환기율은 적정 실내외 기온차에서의 값을 제시할 필요가 있고, 최대난방부하 산정의 기준이 되는 낮은 풍속 범위에서 풍속에 따른 틈새환기율의 변화는 고려하지 않아도 되는 것으로 고찰되었다. 다만 강풍지역에서는 열관류율을 포함하여 최대난방부하를 약간 증가시키는 보정계수의 적용이 필요할 것으로 판단되었다. 온실의 틈새환기전열부하 산정방법을 검토한 결과 틈새환기전열계수와 온실의 피복면적을 이용하는 방법은 문제가 있는 것으로 나타났으며, 틈새환기율과 온실의 체적을 이용하는 방법이 합리적인 것으로 판단되었다.

• Nuclear Engineering and Technology
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• 제25권1호
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• pp.91-101
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• 1993

가압경수로형 원자로의 정상 비정상 운전시의 열수력학적 거동을 예측하기 위해서는 원자로내기포계수의 분포를 정확히 계산하는 것이 필수적이다. 이러한 기포계수의 정확한 예측을 위하여 많은 모델들이 제시되었다. 이중 drift-flux모델은 그 계산의 정확성과 간결성에 의하여 널리 사용되고 있다. 이러한 drift-flux 모델을 사용하여 보다 더 정확한 기포계수를 예측하기 위해서는 각 상간의 슬립률과 flow regime 에 따른 기포의 운동의 변화가 정확히 고려되어야 한다. Drift-flux 모델에서는 이러한 두 가지 요소가 drift-flux parameter인 $C_{o}$ 와 (equation omitted), 에서 고려된다. 본 연구에서는 이러한 $C_{o}$ 의 실험적 결정을 위하여 원자로 노심을 모사한 4개의 전열봉이 있는 비등이 발생하는 수직사각 유로를 구성하였으며, 완성된 유로내에서 기포계수의 분포 및 기포속도의 분포를 측정하였다. 국부적 기포계수 및 기포속도 분포의 측정에 사용된 방법은 이중탐침법이며 측정이 이루어진 유로내의 유동 상태는 유속이 비교적 느린 low flow rate condition이며 유로내 압력은 3기압 이하이다. 본 실험에서는 액상의 속도는 측정되지 않았으며, 따라서 $C_{o}$ 의 계산을 위하여 (equation omitted)의 실험 상관관계식을 사용하여 유로내 평균 기포계수의 함수로 나타내었다.